WO2022170373A1 - Procédé de pulpage mécanique assisté chimiquement de copeaux de bois ou de chutes de bois - Google Patents
Procédé de pulpage mécanique assisté chimiquement de copeaux de bois ou de chutes de bois Download PDFInfo
- Publication number
- WO2022170373A1 WO2022170373A1 PCT/AT2022/060028 AT2022060028W WO2022170373A1 WO 2022170373 A1 WO2022170373 A1 WO 2022170373A1 AT 2022060028 W AT2022060028 W AT 2022060028W WO 2022170373 A1 WO2022170373 A1 WO 2022170373A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- wood
- wood chips
- solvent
- feedstock
- wood chip
- Prior art date
Links
- 239000002023 wood Substances 0.000 title claims abstract description 60
- 238000000034 method Methods 0.000 title claims abstract description 56
- 238000004537 pulping Methods 0.000 title claims abstract description 15
- 230000005496 eutectics Effects 0.000 claims abstract description 32
- 238000000227 grinding Methods 0.000 claims abstract description 23
- 239000002904 solvent Substances 0.000 claims abstract description 23
- 239000006184 cosolvent Substances 0.000 claims abstract description 9
- 150000003242 quaternary ammonium salts Chemical class 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 230000008569 process Effects 0.000 claims description 34
- 239000011111 cardboard Substances 0.000 claims description 10
- 239000001763 2-hydroxyethyl(trimethyl)azanium Substances 0.000 claims description 9
- 235000019743 Choline chloride Nutrition 0.000 claims description 9
- SGMZJAMFUVOLNK-UHFFFAOYSA-M choline chloride Chemical compound [Cl-].C[N+](C)(C)CCO SGMZJAMFUVOLNK-UHFFFAOYSA-M 0.000 claims description 9
- 229960003178 choline chloride Drugs 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- 239000011087 paperboard Substances 0.000 claims description 8
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 7
- 239000004202 carbamide Substances 0.000 claims description 7
- 150000001408 amides Chemical class 0.000 claims description 5
- DLFVBJFMPXGRIB-UHFFFAOYSA-N Acetamide Chemical compound CC(N)=O DLFVBJFMPXGRIB-UHFFFAOYSA-N 0.000 claims description 4
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 claims description 4
- 125000001500 prolyl group Chemical class [H]N1C([H])(C(=O)[*])C([H])([H])C([H])([H])C1([H])[H] 0.000 claims description 4
- 239000004381 Choline salt Substances 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 235000019417 choline salt Nutrition 0.000 claims description 3
- 150000003248 quinolines Chemical class 0.000 claims description 3
- VTVJMWZZVJSEMO-BYPYZUCNSA-N (2s)-pyrrolidine-2-carbonyl chloride Chemical compound ClC(=O)[C@@H]1CCCN1 VTVJMWZZVJSEMO-BYPYZUCNSA-N 0.000 claims description 2
- 239000000654 additive Substances 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 239000008394 flocculating agent Substances 0.000 claims description 2
- 230000014759 maintenance of location Effects 0.000 claims description 2
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 claims 1
- 239000007844 bleaching agent Substances 0.000 claims 1
- 238000004513 sizing Methods 0.000 claims 1
- 239000010875 treated wood Substances 0.000 claims 1
- 229920001131 Pulp (paper) Polymers 0.000 description 26
- 239000000835 fiber Substances 0.000 description 24
- 229920005610 lignin Polymers 0.000 description 15
- 239000000126 substance Substances 0.000 description 13
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 11
- 239000000123 paper Substances 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 9
- 101000952234 Homo sapiens Sphingolipid delta(4)-desaturase DES1 Proteins 0.000 description 8
- 102100037416 Sphingolipid delta(4)-desaturase DES1 Human genes 0.000 description 8
- 101100322245 Caenorhabditis elegans des-2 gene Proteins 0.000 description 5
- 238000010009 beating Methods 0.000 description 5
- 238000011161 development Methods 0.000 description 5
- 230000029087 digestion Effects 0.000 description 5
- 238000005265 energy consumption Methods 0.000 description 5
- 230000009467 reduction Effects 0.000 description 5
- 229920002488 Hemicellulose Polymers 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 235000011187 glycerol Nutrition 0.000 description 4
- 239000002655 kraft paper Substances 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000007858 starting material Substances 0.000 description 4
- 238000010025 steaming Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 238000004182 chemical digestion Methods 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- WQZGKKKJIJFFOK-QTVWNMPRSA-N D-mannopyranose Chemical compound OC[C@H]1OC(O)[C@@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-QTVWNMPRSA-N 0.000 description 2
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 2
- 206010016807 Fluid retention Diseases 0.000 description 2
- 241000218657 Picea Species 0.000 description 2
- 235000008124 Picea excelsa Nutrition 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000001311 chemical methods and process Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- JJCWKVUUIFLXNZ-UHFFFAOYSA-M 2-hydroxyethyl(trimethyl)azanium;bromide Chemical compound [Br-].C[N+](C)(C)CCO JJCWKVUUIFLXNZ-UHFFFAOYSA-M 0.000 description 1
- 229920003043 Cellulose fiber Polymers 0.000 description 1
- AEMOLEFTQBMNLQ-YMDCURPLSA-N D-galactopyranuronic acid Chemical compound OC1O[C@H](C(O)=O)[C@H](O)[C@H](O)[C@H]1O AEMOLEFTQBMNLQ-YMDCURPLSA-N 0.000 description 1
- IAJILQKETJEXLJ-UHFFFAOYSA-N Galacturonsaeure Natural products O=CC(O)C(O)C(O)C(O)C(O)=O IAJILQKETJEXLJ-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- FRYDSOYOHWGSMD-UHFFFAOYSA-N [C].O Chemical compound [C].O FRYDSOYOHWGSMD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 description 1
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000012511 carbohydrate analysis Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 229960001231 choline Drugs 0.000 description 1
- OEYIOHPDSNJKLS-UHFFFAOYSA-N choline Chemical compound C[N+](C)(C)CCO OEYIOHPDSNJKLS-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000012978 lignocellulosic material Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000000930 thermomechanical effect Effects 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/02—Pretreatment of the finely-divided materials before digesting with water or steam
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/02—Pretreatment of the raw materials by chemical or physical means
- D21B1/021—Pretreatment of the raw materials by chemical or physical means by chemical means
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/10—Physical methods for facilitating impregnation
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/006—Pulping cellulose-containing materials with compounds not otherwise provided for
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/20—Pulping cellulose-containing materials with organic solvents or in solvent environment
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/222—Use of compounds accelerating the pulping processes
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/001—Modification of pulp properties
- D21C9/002—Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives
- D21C9/005—Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives organic compounds
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/001—Modification of pulp properties
- D21C9/007—Modification of pulp properties by mechanical or physical means
Definitions
- the present invention relates to a process for a chemically assisted mechanical pulping process for wood chips or wood chips and to paper or cardboard produced therewith.
- wood chips or wood chips In order to obtain a suitable starting material for the production of paper, cardboard or cellulose, two different pulping processes for wood chips or wood chips are usually used in industry.
- the so-called kraft process is usually used for the chemical digestion of wood chips.
- wood chips or wood chips can be broken down using what is known as a semi-chemical or semi-chemical digestion process, in which a two-stage process is used.
- thermo-mechanical digestion In addition to these two processes for breaking down wood chips or wood chips, a hybrid of the two known processes, the so-called thermo-mechanical digestion, is used, which is characterized on the one hand by a very high energy consumption and on the other hand leads to a and cardboard production leads to particularly well-suited wood pulp.
- a method has already become known from EP 2 876 202 A1, which replaces at least part of the chemical batch in a conventional semi-chemical wood pulping process or also chemical wood pulping process by using a so-called strong eutectic solvent in order to achieve improved separation of lignin and lignocellulose as a result of the pulping process.
- the strongly eutectic solvents used in this document are described, for example, in WO 2013/153203 A1 and consist of a salt in its liquid state that consists of a mixture of a proton donor and a proton acceptor, which mixture contains a eutectic with a forms a low melting point, which melting point is significantly lower than that of the individual components.
- various examples of strongly eutectic solvents can be found in the document and that these can be used in connection with lignocellulosic starting materials, in particular for dissolving the lignin contained in these materials.
- pulp suspensions of this type are usually subjected to beating in order to comminute unopened or only partially open wood particles to such an extent that they do not lead to any inhomogeneities in the product made from the wood pulp.
- the disadvantage of grinding is that, in addition to the comminution of unbroken-up wood particles, a not inconsiderable part of the fibers of the input material is also ground up and thus be shortened, so that a final product after grinding has a fiber length distribution corresponding to a Gaussian curve, which is shifted in the direction of shorter fibers in relation to the fiber length of the heating material used.
- the presence of longer fibers in the lignocellulosic material has the advantage that a better lattice network can be formed in the paper web and consequently, for example, papers with increased stretchability according to ISO 1924-3 can be obtained.
- a chemically assisted mechanical pulping process for wood chips which essentially has the following steps: a) producing a feed material from wood chips; b) contacting the wood chip feedstock with steam at a first pressure of between 1 and 2 bar, a steam temperature of between 100 and 110°C for a period of between 10 and 20 minutes to produce a steamed wood chip feedstock; c) contacting the vaporized wood chip feedstock with a solution containing a strong eutectic solvent comprising a quaternary ammonium salt and a co-solvent at a temperature between 40 and 120°C, preferably 50 to 100 ° C and for a time between 5 and 15 minutes, preferably 5 to 10 minutes to obtain a pretreated wood chip feedstock having a strong eutectic solvent concentration greater than 92 mass.
- -% preferably greater than 95% by mass, is selected and a remainder of the solution consists essentially of water, and wherein a molar ratio of the quaternary ammonium salt to a co-solvent is selected between 1:1 and 1:2; and d) mechanically grinding the pretreated wood chip feedstock at a pressure between 1 and 3.5 bar and a temperature above 100°C.
- a further advantage of such a procedure is that the strongly eutectic solvent is kept at the lowest possible temperature and thus on the one hand the energy balance can be optimized and on the other hand any adverse effects on the plant, in particular its tendency to corrode or deterioration, are minimized as far as possible - ten can be, in that the eutectic solvent used is not corrosive, in contrast to the strong bases and acids usually used, corrosion of the ⁇ niagenteie can be prevented, for example, and the use of stainless steel for plant construction can be avoided as a result. This also makes it possible to prevent unwanted discoloration of the paper or cardboard web due to corroded plant parts.
- the process is carried out in such a way that the grinding in step d) is carried out at a temperature between 100 and 160° C., in particular at a temperature which increases from 115° to around 150° C. in the course of the grinding, by Temperature is gradually raised during grinding in step d).
- the method is conducted in such a way that the pressure in the grinding step is also increased successively from values of 1.0 to 2.5 or 3.0 or 3.5 bar.
- the method is carried out in such a way that a choline salt or a proline salt is used as the quaternary ammonium salt. If a choline or proline salt is used, a strongly eutectic solvent can be provided which shows a particularly strong reduction in the melting point and thus allows the process to be carried out at low temperatures and relatively low energy consumption.
- the choline salt used is a choline chloride or choline bromide or the proline salt is a proline chloride
- an amide is used as a co-solvent, in particular an amide selected from the group consisting of urea, formamide and acetamide, which amides are strongly basic on the one hand and thus make the digestion process significantly easier and on the other hand also result in a significant reduction in the melting point of the ammonium salt and thus contribute to a strong or deep eutectic.
- urea is particularly preferred for ecological reasons, since waste products containing urea can be landfilled or even used, for example, as fertilizer for forests or the like.
- the invention also relates to the use of wood chips or wood chips produced according to the method of the invention and of auxiliaries and additives selected from the group of wet strength agents, flocculants, sizes, retention aids and bleaches for the production of paper or cardboard.
- Paper or cardboard produced using wood chips or wood chips produced in this way has particularly homogeneous fibers and thus constant properties over the entire length or width of the paper produced.
- the fiber length is significantly longer than that of conventionally produced papers and the papers also have significantly reduced air permeability, they can be used without special or additional surface treatment, particularly in cases where a particularly dense material is desired.
- the invention is explained in more detail below using exemplary embodiments.
- wood chips or wood chips that were produced from Norway spruce (Picea abies) using a reduction device, for example a chipper were used.
- the wood chips were subjected to steaming, which steaming for a period of 10 minutes at a pressure of at least 1.0 bar, in particular a pressure between 1.0 and 1.5 bar and a steam temperature of over 100° C, advantageously around 110 °C.
- the purpose of steaming is to remove air from the wood chips or the wood chips as well as to raise the temperature of the wood chips and to stabilize it at the selected level.
- the chips were soaked in a strong eutectic solvent.
- the steamed wood chips were soaked at 50 °C and at 70 °C in the strongly eutectic solution consisting of choline chloride and urea as well as that consisting of choline chloride and glycerine.
- the wood chips or wood chips obtained in this way were fed to a grinding device or a refiner and subjected to a grinding process there as follows: water was injected in a preheating stage in order to adjust a wood pulp to a mass content of 25%. The grinding was then started and the temperature was gradually increased from an initial temperature of 100° C. to 150° C. and the pressure in the grinding chamber was raised in the same way from 1 bar to at least 3.0 bar, in particular 3.5 bar. The grinding was continued until the specific energy consumption reached 2,000 kWh/t.
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Paper (AREA)
- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
Abstract
L'invention concerne un procédé de pulpage mécanique assisté chimiquement de copeaux de bois, ledit procédé consistant : a) à produire une charge d'alimentation à partir de copeaux de bois ; b) à mettre la charge d'alimentation en contact avec de la vapeur à une pression comprise entre 1 et 2 bars et une température de vapeur comprise entre 100 et 110 °C pendant 10 à 20 minutes afin de produire une charge d'alimentation de copeaux de bois traitée à la vapeur ; c) à mettre la charge de copeaux de bois traitée à la vapeur en contact avec une solution contenant un solvant eutectique profond comprenant un sel d'ammonium quaternaire et un co-solvant entre 40 et 120 °C et pendant 5 et 15 minutes afin d'obtenir une charge d'alimentation de copeaux de bois prétraitée, une concentration du solvant eutectique profond étant supérieure à 92 % en poids et une quantité résiduelle de la solution consistant essentiellement en eau, et dans laquelle un rapport molaire du sel d'ammonium quaternaire à un co-solvant est choisi pour être compris entre 1:1 et 1:2 ; et d) à broyer mécaniquement la charge d'alimentation de copeaux de bois prétraitée à une pression comprise entre 1 et 3,5 bars et à une température supérieure à 100 °C. L'invention concerne également un papier ou une plaque produits à l'aide de ce dernier.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP22702851.1A EP4291708A1 (fr) | 2021-02-12 | 2022-01-31 | Procédé de pulpage mécanique assisté chimiquement de copeaux de bois ou de chutes de bois |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ATA50089/2021A AT524693B1 (de) | 2021-02-12 | 2021-02-12 | Verfahren für ein chemisch unterstütztes mechanisches Aufschlussverfahren von Hackschnitzeln bzw. Hackspänen |
ATA50089/2021 | 2021-02-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2022170373A1 true WO2022170373A1 (fr) | 2022-08-18 |
Family
ID=80222425
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AT2022/060028 WO2022170373A1 (fr) | 2021-02-12 | 2022-01-31 | Procédé de pulpage mécanique assisté chimiquement de copeaux de bois ou de chutes de bois |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP4291708A1 (fr) |
AT (1) | AT524693B1 (fr) |
WO (1) | WO2022170373A1 (fr) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013153203A1 (fr) | 2012-04-12 | 2013-10-17 | Technische Universiteit Eindhoven | Prétraitement de biomasse lignocellulosique et récupération de substituants au moyen de mélanges naturels de solvants eutectiques profonds (des)/composés présentant des températures de transition basses |
EP2876202A1 (fr) | 2013-11-25 | 2015-05-27 | CEPI aisbl | Utilisation de solvants eutectiques profonds dans la production de papier |
EP3023539A1 (fr) * | 2014-11-18 | 2016-05-25 | UPM-Kymmene Corporation | Procédé de production de pulpe |
WO2017032926A2 (fr) * | 2015-08-27 | 2017-03-02 | Teknologian Tutkimuskeskus Vtt Oy | Procédé de conversion de biomasse |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI129866B (fi) * | 2019-05-15 | 2022-10-14 | Lappeenrannan Lahden Teknillinen Yliopisto Lut | Menetelmä lignoselluloosamateriaalin fraktioimiseksi ja mainitulla menetelmällä saadut tuotteet |
AU2020100319A4 (en) * | 2020-03-04 | 2020-05-14 | Qilu University Of Technology | Method for preparing cellulose nanofibrils by deep eutectic solvent pretreatment |
CN112431055A (zh) * | 2020-11-16 | 2021-03-02 | 陕西科技大学 | 一种由造纸用化学浆制备溶解浆的新工艺 |
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2021
- 2021-02-12 AT ATA50089/2021A patent/AT524693B1/de active
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2022
- 2022-01-31 WO PCT/AT2022/060028 patent/WO2022170373A1/fr active Application Filing
- 2022-01-31 EP EP22702851.1A patent/EP4291708A1/fr active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013153203A1 (fr) | 2012-04-12 | 2013-10-17 | Technische Universiteit Eindhoven | Prétraitement de biomasse lignocellulosique et récupération de substituants au moyen de mélanges naturels de solvants eutectiques profonds (des)/composés présentant des températures de transition basses |
EP2876202A1 (fr) | 2013-11-25 | 2015-05-27 | CEPI aisbl | Utilisation de solvants eutectiques profonds dans la production de papier |
EP3023539A1 (fr) * | 2014-11-18 | 2016-05-25 | UPM-Kymmene Corporation | Procédé de production de pulpe |
WO2017032926A2 (fr) * | 2015-08-27 | 2017-03-02 | Teknologian Tutkimuskeskus Vtt Oy | Procédé de conversion de biomasse |
Non-Patent Citations (1)
Title |
---|
PRATIMA BAJPAI: "Bierman's Handbook of Pulp and Paper: raw material and Pulp making", 2018, ELSEVIER AMSTERDAM |
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AT524693A1 (de) | 2022-08-15 |
AT524693B1 (de) | 2022-11-15 |
EP4291708A1 (fr) | 2023-12-20 |
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